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Catalyst for production of isobutene through dehydrogenation of isobutane and application thereof

A technology for producing isobutylene and catalysts, which is applied in the direction of catalysts, carbon compound catalysts, metal/metal oxides/metal hydroxide catalysts, etc., can solve the problems of catalyst activity reduction and achieve good technical effects

Active Publication Date: 2019-04-19
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

When La is excessive, Pt aggregates and Sn also becomes metal, resulting in a decrease in catalyst activity
[0004] Isobutane dehydrogenation catalysts have made great progress, but there is still room for improvement in catalyst activity
The present invention adopts M1-M2-Al-O as the carrier to load Pt-Sn catalyst to improve the performance of the catalyst, and has good application prospect, but there is no relevant report yet

Method used

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  • Catalyst for production of isobutene through dehydrogenation of isobutane and application thereof
  • Catalyst for production of isobutene through dehydrogenation of isobutane and application thereof
  • Catalyst for production of isobutene through dehydrogenation of isobutane and application thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0031] Weigh 39.97g of beryllium chloride, 110.59g of indium chloride, 49.05g of lanthanum chloride and 240.01g of soluble salt of aluminum chloride and dissolve them in 1L of deionized water, mix well, and slowly drip ammonia water under continuous stirring, Adjust the pH value to 8.5, age the product for 2 hours, filter and wash with 4L of water to obtain a filter cake, dry the filter cake at 90°C for 16 hours, and roast it in a muffle furnace at 580°C for 20 hours to obtain Be 0.5 In 0.5 La 0.2 Al 1.8 o x carrier. Weigh 9.86g of carrier and put it into a beaker, then weigh 0.190g of stannous chloride and dissolve it in 10mL of hydrochloric acid solution, add the above-mentioned carrier under stirring, mix well, soak at 30°C for 12 hours, and then dry at 90°C for 16 hours Obtain catalyst precursor, denoted as I. Weigh 0.106g of chloroplatinic acid and dissolve it in 10mL of water, add it into I while stirring, mix evenly, soak at 30°C for 12 hours, dry at 90°C for 16 ho...

Embodiment 2

[0033]Weigh 128.2g of magnesium nitrate, 190.96g of indium nitrate, 64.98g of lanthanum nitrate and 675.23g of soluble salt of aluminum nitrate, dissolve them in 1L of deionized water, mix well, and slowly add ammonia water under continuous stirring to adjust the pH value 8.5, aged the product for 2 hours, filtered and washed with 4L of water to obtain a filter cake, dried the filter cake at 90°C for 16 hours, and roasted it in a muffle furnace at 580°C for 20 hours to obtain Mg 0.5 In 0.5 La 0.2 Al 1.8 o x carrier. Weigh 9.86g of carrier and put it into a beaker, then weigh 0.190g of stannous chloride and dissolve it in 10mL of hydrochloric acid solution, add the above-mentioned carrier under stirring, mix well, soak at 30°C for 12 hours, and then dry at 90°C for 16 hours Obtain catalyst precursor, denoted as I. Weigh 0.106g of chloroplatinic acid and dissolve it in 10mL of water, add it into I while stirring, mix evenly, soak at 30°C for 12 hours, dry at 90°C for 16 hou...

Embodiment 3

[0035] Weigh 88.09g of calcium acetate, 194.97g of indium acetate, 63.21g of lanthanum acetate and 291.75g ​​of basic aluminum acetate soluble salt, dissolve them in 1L of deionized water, mix well, and slowly add ammonia water dropwise under continuous stirring to adjust the pH The value is 8.5, the product is aged for 2 hours, filtered and washed with 4L of water to obtain a filter cake, dried at 90°C for 16 hours, and then roasted in a muffle furnace at 580°C for 20 hours to obtain Ca 0.5 In 0.5 La 0.2 Al 1.8 o x carrier. Weigh 9.86g of carrier and put it into a beaker, then weigh 0.190g of stannous chloride and dissolve it in 10mL of hydrochloric acid solution, add the above-mentioned carrier under stirring, mix well, soak at 30°C for 12 hours, and then dry at 90°C for 16 hours Obtain catalyst precursor, denoted as I. Weigh 0.106g of chloroplatinic acid and dissolve it in 10mL of water, add it into I while stirring, mix evenly, soak at 30°C for 12 hours, dry at 90°C f...

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Abstract

The invention relates to a catalyst for production of isobutene through dehydrogenation of isobutane and application thereof, and mainly solves the problem that the activity of a dehydrogenation catalyst prepared in the prior art is low. The composition catalyst comprises the following components in parts by weight: a) 0.1-5 parts of Pt or an oxide thereof; b) 0.1-5 parts of Sn or an oxide thereof; and c) 90-99 parts of a compound oxide M1-M2-Al-O carrier, M1 is selected from a mixture of IIA and IIIA elements, M2 is selected from at least one of lanthanide elements, and the catalyst can wellsolve the problem that the activity of the dehydrogenation catalyst prepared in the prior art is low, and can be used for industrial production of isobutene through dehydrogenation of isobutane.

Description

technical field [0001] The invention relates to a catalyst for preparing isobutene from isobutane dehydrogenation and its application. Background technique [0002] Isobutylene is an important chemical raw material, mainly used to produce polyisobutylene, butyl rubber and methyl tert-butyl ether (MTBE). MTBE is a high-octane liquid that is often used to increase the octane number of gasoline Additives, the market demand is relatively large, which drives the development and utilization of MTBE upstream products. The content of isobutane in the mixed C4 by-product of catalytic cracking unit is as high as 45.5%, and most enterprises directly sell isobutane as liquefied gas. With the continuous expansion of the scale of domestic oil refining units and catalytic cracking units, the production capacity of isobutane will be further increased in the future, and how to improve the economic benefits of isobutane has gradually become a hot spot in the utilization of C4 resources. Usi...

Claims

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Application Information

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IPC IPC(8): B01J23/63C07C5/333C07C11/09
CPCB01J23/002B01J23/63B01J2523/00C07C5/3332C07C2523/63B01J2523/21B01J2523/31B01J2523/33B01J2523/3706B01J2523/43B01J2523/828B01J2523/22B01J2523/23B01J2523/24B01J2523/25C07C11/09
Inventor 姜冬宇缪长喜吴文海曾铁强张新玉
Owner CHINA PETROLEUM & CHEM CORP